WO2008022802A1 - Film soufflé de polypropylène - Google Patents

Film soufflé de polypropylène Download PDF

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Publication number
WO2008022802A1
WO2008022802A1 PCT/EP2007/007468 EP2007007468W WO2008022802A1 WO 2008022802 A1 WO2008022802 A1 WO 2008022802A1 EP 2007007468 W EP2007007468 W EP 2007007468W WO 2008022802 A1 WO2008022802 A1 WO 2008022802A1
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WO
WIPO (PCT)
Prior art keywords
polypropylene
blown film
shi
film
strain
Prior art date
Application number
PCT/EP2007/007468
Other languages
English (en)
Inventor
Manfred Stadlbauer
Eberhard Ernst
Peter Niedersüss
Original Assignee
Borealis Technology Oy
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Borealis Technology Oy filed Critical Borealis Technology Oy
Priority to DE602007004630T priority Critical patent/DE602007004630D1/de
Priority to EA200970221A priority patent/EA200970221A1/ru
Priority to BRPI0717001-7A priority patent/BRPI0717001A2/pt
Priority to AT07801893T priority patent/ATE456608T1/de
Priority to CN2007800290360A priority patent/CN101501110B/zh
Priority to EP07801893A priority patent/EP2054464B1/fr
Publication of WO2008022802A1 publication Critical patent/WO2008022802A1/fr
Priority to US12/367,799 priority patent/US20090182105A1/en

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29D—PRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D7/00—Producing flat articles, e.g. films or sheets
    • B29D7/01—Films or sheets
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18—Manufacture of films or sheets
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/10—Homopolymers or copolymers of propene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/10—Homopolymers or copolymers of propene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/16—Elastomeric ethene-propene or ethene-propene-diene copolymers, e.g. EPR and EPDM rubbers

Definitions

  • the present invention relates to new blown films comprising polypropylene and its manufacture.
  • Polypropylenes succeed more and more to replace polyethylenes in many technical fields as quite often the new generation of polypropylenes have enhanced properties compared to conventional polyethylene materials. This applies also for the field of blown films where polypropylene take advantage of molecular engineering to overcome previous material shortcomings for blown-film production.
  • polypropylene take advantage of molecular engineering to overcome previous material shortcomings for blown-film production.
  • Such polypropylenes are inter alia characterized by a rather high viscosity, i.e. by a rather high molecular mass. The high viscosity improves the strain-hardening elongational viscosity performance.
  • the object of the present invention is to provide a blown film with good mechanical properties, like a high stiffness, based on a polymer, preferably on a polypropylene, which can be converted in a blown film with high output rates. It is in particular preferred that the blown film can be used for food and/or medical packaging without the risk of heat damage and/or without the risk of contamination of said products.
  • the finding of the present invention is to provide a blown film based on polypropylene being multi-branched, i.e. not only the polypropylene backbone is furnished with a larger number of side chains (branched polypropylene) but also some of the side chains themselves are provided with further side chains.
  • the present invention is related, in a first embodiment, to a blown film comprising a polypropylene, wherein said polypropylene is produced in the presence of a metallocene catalyst, preferably in the presence of a metallocene catalyst as further defined below, and said film and/or said polypropylene has (have) a. a branching index g' of less than 1.00 and b.
  • the strain hardening index (SHI) is defined as the slope of the logarithm to the basis 10 of the tensile stress growth function (Ig ( ⁇ + )) as function of the logarithm to the basis 10 of the Hencky strain (Ig ( ⁇ )) in the range of Hencky strains between 1 and 3.
  • the blown film is free of polyethylene, even more preferred the blown film comprises a polypropylene as defined above and further defined below as the only polymer component.
  • the melt of the film in the extrusion process has a high stability, i.e. the extrusion line can be operated at a high screw speed (see Figure 6).
  • the inventive blown film is characterized by a rather high stiffness at a low heat sealing initiation temperature (SIT) in comparison to polymers being state of the art.
  • the inventive blown films are characterized by good optical properties.
  • one characteristic of the blown film and/or the polypropylene component of the inventive film according to the present invention is in particular its (their) extensional melt flow properties.
  • the extensional flow, or deformation that involves the stretching of a viscous material is the dominant type of deformation in converging and squeezing flows that occur in typical polymer processing operations.
  • Extensional melt flow measurements are particularly useful in polymer characterization because they are very sensitive to the molecular structure of the polymeric system being tested.
  • the true strain rate of extension also referred to as the Hencky strain rate
  • simple extension is said to be a "strong flow” in the sense that it can generate a much higher degree of molecular orientation and stretching than flows in simple shear.
  • extensional flows are very sensitive to crystallinity and macro-structural effects, such as long-chain branching, and as such can be far more descriptive with regard to polymer characterization than other types of bulk rheological measurement which apply shear flow.
  • the polypropylene of the blown film has a branching index g' of less than 1.00, more preferably less than 0.90, still more preferably less than 0.80.
  • the branching index g' shall be less than 0.75, i.e. 0.7 or less.
  • the branching index g' is more than 0.6, still more preferably 0.7 or more.
  • the branching index g' of the polypropylene is in the range of 0.6 to below 1.0, more preferred in the range of more than 0.65 to 0.95, still more preferred in the range of 0.7 to 0.95.
  • the branching index g' defines the degree of branching and correlates with the amount of branches of a polymer.
  • a low g'-value is an indicator for a high branched polymer. In other words, if the g'-value decreases, the branching of the polypropylene increases.
  • the branching index g' is preferably of less than 1.00, more preferably less than 0.90, still more preferably less than 0.80. In the preferred embodiment, the branching index g' of the blown film shall be less than 0.75, i.e. 0.7 or less.
  • the intrinsic viscosity needed for determining the branching index g 1 is measured according to DIN ISO 1628/1 , October 1999 (in Decalin at 135 0 C).
  • strain hardening index (SHI@l s ' ') of the polypropylene of the blown film shall be at least 0.30, more preferred of at least 0.40, still more preferred of at least 0.50. In a preferred embodiment the strain hardening index (SHI@l s " ') is at least 0.55.
  • the strain hardening index is a measure for the strain hardening behavior of the polymer melt, in particular the polypropylene melt.
  • the strain hardening index (SHI@l s " ') has been measured by a deformation rate d ⁇ /dt of 1.00 s "1 at a temperature of 180 °C for determining the strain hardening behavior, wherein the strain hardening index (SHI) is defined as the slope of the tensile stress growth function ⁇ + as a function of the Hencky strain f on a logarithmic scale between 1.00 and 3.00 (see figure 1).
  • Lo is the fixed, unsupported length of the specimen sample being stretched which is equal to the centerline distance between the master and slave drums
  • R is the radius of the equi-dimensional windup drums
  • ⁇ is a constant drive shaft rotation rate
  • ⁇ ( ⁇ ) F( ⁇ ) with ⁇ H - A( ⁇ )
  • T is the measured torque signal, related to the tangential stretching force "F”
  • A is the instantaneous cross-sectional area of a stretched molten specimen
  • Ao is the cross-sectional area of the specimen in the solid state (i.e. prior to melting)
  • d s is the solid state density
  • 'M M the melt density of the polymer.
  • the strain hardening index (SHl@ls ⁇ ') is preferably at least 0.30, more preferred of at least 0.40, yet more preferred the strain hardening index (SHI@ls ⁇ ') is of at least 0.40. In a preferred embodiment the strain hardening index (SHI@l s " ') is at least 0.55.
  • MBI multi- branching index
  • a strain hardening index (SHI) is defined as the slope of the logarithm to the basis 10 of the tensile stress growth function ⁇ g + , Ig( ⁇ t + ), as function of the logarithm to the basis 10 of the Hencky strain ⁇ , ⁇ g( ⁇ ), between Hencky strains 1.00 and 3.00 at a at a temperature of 180 °C, where a SHI@0.1 s '1 is determined with a deformation rate ⁇ H of 0.10 s "1 , a SHI@0.3 s "1 is determined with a deformation rate ⁇ H of 0.30 s "1 , a SHI@3 s '1 is determined with a deformation rate ⁇ H of 3.00 s "1 , and a SHI@10 s "1 is determined with a deformation rate ⁇ H of 10.0 s
  • a multi-branching index is defined as the slope of the strain hardening index (SHI) as a function of Ig ( ⁇ H ), i.e.
  • the strain hardening index (SHI) is defined at deformation rates ⁇ H between 0.05 s "1 and 20.00 more preferably between 0.10 s "1 and 10.00 s "1 , still more preferably at the deformations rates 0.10, 0.30, 1.00, 3.00 and 10.00 s "1 . Yet more preferably the SHI- values determined by the deformations rates 0.10, 0.30, 1.00, 3.00 and 10.00 s "1 are used for the linear fit according to the least square method when establishing the multi-branching index (MBI).
  • MBI multi-branching index
  • the blown film and/or the polypropylene of said film has a multi-branching index (MBI) of at least 0.15, more preferably of at least 0.20, and still more preferred of at least 0.25.
  • the multi-branching index (MBI) is at least 0.28.
  • the blown film and/or the polypropylene of said film has (have) a branching index g' of less than 1.00, a strain hardening index (SHI@l s " ') of at least 0.30 and multi-branching index (MBI) of at least 0.15. Still more preferred the blown film and/or the polypropylene of said film has (have) a branching index g' of less than 0.80, a strain hardening index (SHI@l s ' ') of at least 0.40 and multi-branching index (MBI) of at least 0.15.
  • the blown film and/or the polypropylene of said film has (have) a branching index g' of less than 1.00, a strain hardening index (SHI@l s ' ') of at least 0.30 and multi-branching index (MBI) of at least 0.20.
  • the blown film and/or the polypropylene of said film has (have) a branching index g' of less than 0.80, a strain hardening index (SHI@l s ' ') of at least 0.40 and multi- branching index (MBI) of at least 0.20.
  • the blown film and/or the polypropylene of said film has (have) a branching index g' of less than 0.80, a strain hardening index (SHI@l s " ') of at least 0.50 and multi-branching index (MBI) of at least 0.30.
  • inventive blown films and/or the polypropylenes of said film are characterized by the fact that their strain hardening index (SHI) increases with the deformation rate ⁇ H , i.e. a phenomenon which is not observed in other blown films and/or polypropylenes.
  • strain hardening index (SHI) is not influenced by the deformation rate (see Figures 2 and 3). Accordingly, the strain hardening index (SHI) of known polymers, in particular known polypropylenes and polyethylenes, does not increase or increases only negligible with increase of the deformation rate (d ⁇ /dt).
  • the inventive blown film as defined above is characterized in that
  • E IM measured tensile modulus
  • SIT measured heat sealing initiation temperature
  • Said polypropylenes are either propylene homopolymers or polypropylene copolymers, which comprise low amounts of ethylene, i.e. lower than 10 mol%.
  • the properties of said blown films are determined, i.e.
  • the heat sealing initiation temperature (SIT) [°C] as well as the tensile modules (E IM ) [MPa] of the different polypropylenes used in the known blown films in an injection-molded state has been determined (ISO 527-2 (at a speed of 1 mm/min)).
  • the tensile modulus (E IM ) values [MPa] so obtained are plotted against the heat sealing initiation temperature (SIT) values [ 0 C] and thereby - after a linear fit according to the least square method - resulting in a linear relationship, i.e. a linear equation.
  • the blown film comprises a polypropylene homopolymer, i.e. a multi-branched polypropylene homopolymer, as defined in the present invention
  • the sum of SIT and E IM as defined above shall not exceed 90.0.
  • the heat sealing initiation temperature (SIT) of the blown film shall preferably not exceed a specific value, i.e. shall preferably not exceed 140 °C.
  • the heat sealing initiation temperature (SIT) of a film is directly related to the molecular weight and the degree of branching of the polymer.
  • the heat sealing temperatures of the blown film is not higher than 140 °C, still more preferred not higher than 138 °C and yet more preferred not higher than 135 °C.
  • the heat sealing initiation temperatures (SIT) of the blown film and/or the polypropylene of said film is not higher than 140 °C, still more preferred not higher than 138 °C and yet more preferred not higher than 135 °C in case the polypropylene is a propylene homopolymer, i.e. a multi-branched propylene homopolymer, as defined in the present invention.
  • the polypropylene in the blown film is a propylene copolymer, i.e.
  • the heat sealing initiation temperatures (SIT) of the blown film and/or the polypropylene of said film is not higher than 120 °C, still more preferred not higher than 1 18 °C and yet more preferred not higher than 114 °C.
  • the measuring method for the heat sealing initiation temperature (SIT) is defined in the example section.
  • the tensile modulus (E IM ) shall be preferably rather high.
  • the tensile modulus (E IM ) of the blown film and/or the polypropylene of said film in an injection-molded state is at least 1300 MPa, more preferably at least 1400 MPa in case the polypropylene is a propylene homopolymer, i.e. a multi-branched propylene homopolymer, as defined in the present invention.
  • the polypropylene in the blown film is a propylene copolymer, i.e.
  • the tensile modulus (E IM ) of blown film and/or the polypropylene of said film in an injection-molded state is at least 550 MPa, more preferably at least 650 MPa.
  • the tensile modulus of the blown film itself shall be rather high.
  • the tensile modulus of the blown film based on a propylene homopolymer shall be at least 750 MPa, more preferably at least 800 MPa.
  • the heat sealing initiation temperature (SIT) of polymers can be lowered by rather high amount of extractables.
  • extractables are undesirable in the field of food packaging or in the field of medical packaging.
  • the low heat sealing initiation temperature (SIT) values of the blown film are not achieved by adding any plasticizer and/or by using a polypropylene with rather high amounts of comonomers, in particular rather high amounts of ethylene.
  • the comonomer content, preferably the ethylene content, in the polypropylene and/or in the blown film does not exceed 10 mol%, more preferably does not exceed 8 mol%, yet more preferably does not exceed 6 mol%.
  • the polypropylene is a propylene homopolymer as defined below.
  • the blown film does not comprise any plasticizer in detectable amounts.
  • the present invention is related to a blown film comprising a polypropylene, wherein said film and/or said polypropylene has (have) a strain rate thickening which means that the strain hardening increases with extension rates.
  • a strain hardening index (SHI) can be determined at different strain rates.
  • a strain hardening index is defined as the slope of the tensile stress growth function ⁇ + as function of the Hencky strain f on a logarithmic scale between 1.00 and 3.00 at a at a temperature of 180 °C, where a SHI@0.1 s " ' is determined with a deformation rate ⁇ H of 0.10 a SHI@0.3s " ' is determined with a deformation rate ⁇ H of 0.30 s '1 , a SHI@3s '] is determined with a deformation rate ⁇ H of 3.00 s '1 , a SHI@10s " ' is determined with a deformation rate ⁇ H of 10.00 s "1 .
  • a multi-branching index is defined as the slope of the strain hardening index (SHI as a function of Ig ( ⁇ H ), i.e.
  • the strain hardening index (SHI) is defined at deformation rates ⁇ H between 0.05 s "1 and 20.0 s "1 , more preferably between 0.10 s "1 and 10.0 s '1 , still more preferably at the deformations rates 0.10, 0.30, 1.00, 3.00 and 10.0 s " '.Yet more preferably the SHI-values determined by the deformations rates 0.10, 0.30, 1.00, 3.00 and 10.0 s "1 are used for the linear fit according to the least square method when establishing the multi-branching index (MBI).
  • MBI multi-branching index
  • the blown film and/or the polypropylene of said blown film has (have) a multi-branching index (MBI) of at least 0.15.
  • MBI multi-branching index
  • the blown film is free of polyethylene, even more preferred the blown film comprises a polypropylene as defined above and further defined below as the only polymer component.
  • polypropylene is produced in the presence of a metallocene catalyst, more preferably in the presence of a metallocene catalyst as further defined below.
  • the melt of the film in the extrusion process has a high stability, i.e. the extrusion line can be operated at a high screw speed (see Figure 6).
  • the inventive blown film is characterized by a rather high stiffness at a low heat sealing initiation temperature (SIT) in comparison to polymers being sate of the art.
  • the inventive blown films are characterized by good optical properties.
  • one characteristic of the blown film and/or the polypropylene component of the inventive film is (are) in particular the extensional melt flow properties.
  • the extensional flow, or deformation that involves the stretching of a viscous material is the dominant type of deformation in converging and squeezing flows that occur in typical polymer processing operations.
  • Extensional melt flow measurements are particularly useful in polymer characterization because they are very sensitive to the molecular structure of the polymeric system being tested.
  • the true strain rate of extension also referred to as the Hencky strain rate
  • simple extension is said to be a "strong flow” in the sense that it can generate a much higher degree of molecular orientation and stretching than flows in simple shear.
  • extensional flows are very sensitive to crystallinity and macro- structural effects, such as long-chain branching, and as such can be far more descriptive with regard to polymer characterization than other types of bulk rheological measurement which apply shear flow.
  • the first requirement according to the second embodiment is that the blown film and/or the polypropylene of said film has (have) a multi- branching index (MBI) of at least 0.15, more preferably of at least 0.20, and still more preferred of at least 0.30.
  • MBI multi- branching index
  • the multi-branching index is defined as the slope of the strain hardening index (SHI) as a function of Ig (d ⁇ /dt) [d SHI/d Ig (d ⁇ /dt)].
  • the inventive blown film and/or the polypropylene of said film is (are) characterized by the fact that their strain hardening index (SHI) increases with the deformation rate ⁇ H , i.e. a phenomenon which is not observed in other polypropylenes.
  • SHI strain hardening index
  • Single branched polymer types so called Y polymers having a backbone with a single long side-chain and an architecture which resembles a "Y”
  • H-branched polymer types two polymer chains coupled with a bridging group and a architecture which resemble an "H" as well as linear or short chain branched polymers do not show such a relationship, i.e.
  • the strain hardening index (SHI) is not influenced by the deformation rate (see Figures 2 and 3). Accordingly, the strain hardening index (SHI) of known polymers, in particular known polypropylenes and polyethylenes, does not increase or increases only negligible with increase of the deformation rate (d ⁇ /dt). Industrial conversion processes which imply elongational flow operate at very fast extension rates. Hence the advantage of a material which shows more pronounced strain hardening (measured by the strain hardening index (SHI)) at high strain rates becomes obvious. The faster the material is stretched, the higher the strain hardening index (SHI) and hence the more stable the material will be in conversion.
  • the melt of the multi- branched polypropylenes has a high stability.
  • the inventive blown films are characterized by a rather high stiffness even though the sealing temperatures are low.
  • strain hardening index (SHI@l s " ') of the blown film and/or the polypropylene of said film shall be at least 0.30, more preferred of at least 0.40, still more preferred of at least 0.50.
  • the strain hardening index (SHI) is a measure for the strain hardening behavior of the polymer melt, in particular of the polypropylene melt.
  • the strain hardening index (SHI@l s " ') has been measured by a deformation rate (d ⁇ /dt) of 1.00 s "1 at a temperature of 180 °C for determining the strain hardening behavior, wherein the strain hardening index (SHI) is defined as the slope of the tensile stress growth function ⁇ E + as a function of the Hencky strain f on a logarithmic scale between 1.00 and 3.00 (see figure 1).
  • the Hencky strain rate ⁇ H is defined by the formula
  • Lo is the fixed, unsupported length of the specimen sample being stretched which is equal to the centerline distance between the master and slave drums
  • R is the radius of the equi-dimensional windup drums
  • ⁇ is a constant drive shaft rotation rate
  • the Hencky strain rate ⁇ H is defined as for the Hencky strain ⁇ "F" is the tangential stretching force
  • R is the radius of the equi-dimensional windup drums
  • T is the measured torque signal
  • F tangential stretching force
  • A is the instantaneous cross-sectional area of a stretched molten specimen
  • ⁇ o is the cross-sectional area of the specimen in the solid state (i.e. prior to melting)
  • d s is the solid state density and "d M " the melt density of the polymer.
  • the branching index g' of the inventive polypropylene of the bown film shall be less than 1.00, more preferably less than 0.90, still more preferably less than 0.80. In the preferred embodiment, the branching index g' shall be less than 0.75, i.e. 0.70 or less. On the other hand it is preferred that the branching index g' is more than 0.6, still more preferably 0.7 or more. Thus it is preferred that the branching index g' of the polypropylene is in the range of 0.6 to below 1.0, more preferred in the range of more than 0.65 to 0.95, still more preferred in the range of 0.7 to 0.95.
  • the branching index g' defines the degree of branching and correlates with the amount of branches of a polymer.
  • a low g'- value is an indicator for a high branched polymer.
  • the branching index g' is preferably of less than 1.00, more preferably less than 0.90, still more preferably less than 0.80. In the preferred embodiment, the branching index g' of the blown film shall be less than 0.75, i.e. 0.7 or less.
  • the intrinsic viscosity needed for determining the branching index g' is measured according to DIN ISO 1628/1 , October 1999 (in Decalin at 135 0 C).
  • the tensile stress growth function ⁇ + the Hencky strain rate ⁇ H , the Hencky strain ⁇ and the branching index g it is referred to the example section.
  • the inventive blown film and/or the polypropylene of said film has (have) a branching index g' of less than 1.00, a strain hardening index (SHI@ls " ') of at least 0.30 and multi-branching index (MBI) of at least 0.15. Still more preferred the inventive blown film and/or the polypropylene of said film has (have) a branching index g' of less than 0.80, a strain hardening index (SHI@l s * ') of at least 0.40 and multi- branching index (MBI) of at least 0.15.
  • inventive blown film and/or the polypropylene of said film has (have) a branching index g' of less than 1.00, a strain hardening index (SHI@l s " ') of at least 0.30 and multi-branching index (MBI) of at least 020.
  • inventive blown film and/or the polypropylene of said film has (have) a branching index g' of less than 0.80, a strain hardening index (SHI@ l s ' ') of at least 0.40 and multi-branching index (MBI) of at least 020.
  • inventive blown film and/or the polypropylene of said film has (have) a branching index g' of less than 0.80, a strain hardening index (SHI@ls " ') of at least 0.50 and multi-branching index (MBI) of at least 030.
  • the inventive blown film as defined above for the second embodiment is characterized in that a) the heat sealing initiation temperature (SIT) of said film together with the tensile modulus (E IM ) of said film in an injection- molded state measured according to ISO 527-2 (at a speed of 1 mm/min); and/or b) the heat sealing initiation temperature (SIT) of said film together with the tensile modulus (E IM ) of the polypropylene of said film in an injection-molded state measured according to ISO 527-2 (at a speed of 1 mm/min) fulfil(s) the equation
  • E IM measured tensile modulus
  • SIT measured heat sealing initiation temperature
  • Said polypropylenes are either propylene homopolymers or polypropylene copolymers, which comprise low amounts of ethylene, i.e. lower than 10 mol%.
  • the properties of said blown films are determined, i.e.
  • the heat sealing initiation temperature (SIT) [°C] as well as the tensile modules (E IM ) [MPa] of the different polypropylenes used in the known blown films in a injection-molded state has been determined (ISO 527-2 (at a speed of 1 mm/min)).
  • the tensile modulus (E IM ) values [MPa] so obtained are plotted against the heat sealing initiation temperature (SIT) values [ 0 C] and thereby - after a linear fit according to the least square method - resulting in a linear relationship, i.e. a linear equation.
  • the blown film comprises a polypropylene homopolymer, i.e. a multi-branched polypropylene homopolymer, as defined in the present invention the sum of SIT and E I M as defined above shall not exceed 90.0.
  • the heat sealing initiation temperature (SIT) of the blown film shall preferably not exceed a specific value, i.e. shall preferably not exceed 140 °C.
  • the heat sealing initiation temperature (SIT) of a film is directly related to the molecular weight and the degree of branching of the polymer.
  • the heat sealing temperatures of the blown film is not higher than 140 °C, still more preferred not higher than 138 °C and yet more preferred not higher than 135 °C.
  • the heat sealing initiation temperatures (SIT) of the blown film and/or the polypropylene of said film is not higher than 140 0 C, still more preferred not higher than 138 °C and yet more preferred not higher than 135 0 C in case the polypropylene is a propylene homopolymer, i.e. a multi-branched propylene homopolymer, as defined in the present invention.
  • the polypropylene in the blown film is a propylene copolymer, i.e.
  • the heat sealing initiation temperatures (SIT) of the blown film and/or the polypropylene of said film is not higher than 120 0 C, still more preferred not higher than 1 18 0 C and yet more preferred not higher than 1 14 0 C.
  • the measuring method for the heat sealing initiation temperature (SIT) is defined in the example section.
  • the tensile modulus (E IM ) shall be preferably rather high.
  • the tensile modulus (E IM ) of the blown film and/or the polypropylene of said film in an injection-molded state is at least 1300 MPa, more preferably at least 1400 MPa in case the polypropylene is a propylene homopolymer, i.e. a multi-branched propylene homopolymer, as defined in the present invention.
  • the polypropylene in the blown film is a propylene copolymer, i.e.
  • the tensile modulus (E IM ) of blown film and/or the polypropylene of said film in an injection-molded state is at least 550 MPa, more preferably at least 650 MPa.
  • the tensile modulus of the blown film itself shall be rather high.
  • the tensile modulus of the blown film based on a propylene homopolymer shall be at least 750 MPa, more preferably at least 800 MPa.
  • the heat sealing initiation temperature (SIT) of polymers can be lowered by rather high amount of extractables.
  • extractables are undesirable in the field of food packaging or in the field of medical packaging.
  • the low heat sealing initiation temperature (SIT) values of the blown film are not achieved by adding any plasticizer and/or by using a polypropylene with rather high amounts of comonomers, in particular rather high amounts of ethylene.
  • the comonomer content, preferably the ethylene content, in the polypropylene and/or in the blown film does not exceed 10 mol%, more preferably does not exceed 8 mol%, yet more preferably does not exceed 6 mol%.
  • the polypropylene is a propylene homopolymer as defined below.
  • the blown film does not comprise any plasticizer in detectable amounts.
  • the blown film comprises a polypropylene wherein the film is characterized in that a) the heat sealing initiation temperature (SIT) of said film together with the tensile modulus (E IM ) of said film in an injection-molded state measured according to ISO 527-2 (at a speed of 1 mm/min); and/or b) the heat sealing initiation temperature (SIT) of said film together with the tensile modulus (E IM ) of the polypropylene of said film in an injection-molded state measured according to ISO 527-2 (at a speed of 1 mm/min) fulfil(s) the equation SIT [ 0 C] - 0.03 ⁇ E,M [MPa] ⁇ 92.
  • SIT heat sealing initiation temperature
  • E IM tensile modulus
  • the melt of the film in the extrusion process has a high stability, i.e. the extrusion line can be operated at a high screw speed (see Figure 6).
  • the inventive blown film is characterized by a rather high stiffness at a low heat sealing initiation temperature (SIT) in comparison to polymers being sate of the art.
  • the inventive blown films are characterized by good optical properties.
  • E IM measured tensile modulus
  • SIT heat sealing initiation temperature
  • the properties of said blown films are determined, i.e. the heat sealing initiation temperature (SIT) [ 0 C] as well as the tensile modules (E IM ) [MPa] of the different polypropylenes used in the known blown films in a injection-molded state has been determined (ISO 527-2 (at a speed of 1 mm/min)).
  • the tensile modulus (E IM ) values [MPa] so obtained are plotted against the heat sealing initiation temperature (SIT) values [°C] and thereby - after a linear fit according to the least square method - resulting in a linear relationship, i.e. a linear equation.
  • the blown film comprises a polypropylene homopolymer, i.e. a multi-branched polypropylene homopolymer, as defined in the present invention
  • the sum of SIT and E IM as defined above shall not exceed 90.0.
  • the heat sealing initiation temperature (SIT) of the blown film shall preferably not exceed a specific value, i.e. shall preferably not exceed 140 °C.
  • the heat sealing initiation temperature (SIT) of a film is directly related to the molecular weight and the degree of branching of the polymer.
  • the heat sealing temperatures of the blown film is not higher than 140 °C, still more preferred not higher than 138 °C and yet more preferred not higher than 135 °C.
  • the heat sealing initiation temperatures (SIT) of the blown film and/or the polypropylene of said film is not higher than 140 °C, still more preferred not higher than 138 °C and yet more preferred not higher than 135 °C in case the polypropylene is a propylene homopolymer, i.e. a multi-branched propylene homopolymer, as defined in the present invention.
  • the polypropylene in the blown film is a propylene copolymer, i.e.
  • the heat sealing initiation temperatures (SIT) of the blown film and/or the polypropylene of said film is not higher than 120 °C, still more preferred not higher than 118 °C and yet more preferred not higher than 114 °C.
  • the measuring method for the heat sealing initiation temperature (SIT) is defined in the example section.
  • the tensile modulus (E IM ) shall be preferably rather high.
  • the tensile modulus (E IM ) of the blown film and/or the polypropylene of said film in an injection-molded state is at least 1300 MPa, more preferably at least 1400 MPa in case the polypropylene is a propylene homopolymer, i.e. a multi-branched propylene homopolymer, as defined in the present invention.
  • the polypropylene in the blown film is a propylene copolymer, i.e.
  • the tensile modulus (E IM ) of blown film and/or the polypropylene of said film in an injection-molded state is at least 550 MPa, more preferably at least 650 MPa.
  • the tensile modulus of the blown film itself shall be rather high.
  • the tensile modulus of the blown film based on a propylene homopolymer shall be at least 750 MPa, more preferably at least 800 MPa.
  • the heat sealing initiation temperature (SIT) of polymers can be lowered by rather high amount of extractables. However extractables are undesirable in the field of food packaging or in the field of medical packaging.
  • the low heat sealing initiation temperature (SIT) values of the blown film are not achieved by adding any plasticizer and/or by using a polypropylene with rather high amounts of comonomers, in particular rather high amounts of ethylene.
  • the comonomer content, preferably the ethylene content, in the polypropylene and/or in the blown film does not exceed 10 mol%, more preferably does not exceed 8 mol%, yet more preferably does not exceed 6 mol%.
  • the polypropylene is a propylene homopolymer as defined below.
  • the blown film does not comprise any plasticizer in detectable amounts.
  • inventive blown film and/or the polypropylene of said blown film has (have) a strain rate thickening which means that the strain hardening increases with extension rates.
  • a strain hardening index (SHI) can be determined at different strain rates.
  • a strain hardening index is defined as the slope of the tensile stress growth function ⁇ + as function of the Hencky strain ⁇ on a logarithmic scale between 1.00 and 3.00 at a at a temperature of 180 °C, where a SHI@0.1s " ' is determined with a deformation rate ⁇ H of 0.10 s " 1 , a SHI@0.3s " ' is determined with a deformation rate ⁇ H of 0.30 s "1 , a SHI@3s '!
  • a SHI@10s " ' is determined with a deformation rate ⁇ H of 10.0 s ⁇ ⁇
  • the slope of the strain hardening index (SHI) as function of the logarithm to the basis 10 of ⁇ H , Ig ( ⁇ H ) is a characteristic measure for multi -branching. Therefore, a multi-branching index (MBI) is defined as the slope of the strain hardening index (SHI as a function of Ig ( ⁇ H ), i.e.
  • the strain hardening index (SHI) is defined at deformation rates ⁇ H between 0.05 s " 1 and 20.0 s "1 , more preferably between 0.10 s ' 1 and 10.0 s " 1 , still more preferably at the deformations rates 0.10, 0.30, 1.00, 3.00 and 10.00 s ' ' .Yet more preferably the SHI-values determined by the deformations rates 0.10, 0.30, 1.00, 3.00 and 10.00 s "1 are used for the linear fit according to the least square method when establishing the multi-branching index (MBI).
  • MBI multi-branching index
  • the blown film and/or the polypropylene of said blown film has (have) a multi-branching index (MBI) of at least 0.15, more preferably of at least 0.20, and still more preferred of at least 0.30.
  • MBI multi-branching index
  • the blown film and/or the polypropylene component of the inventive film according to the present invention is (are) characterized in particular by extensional melt flow properties.
  • the extensional flow, or deformation that involves the stretching of a viscous material is the dominant type of deformation in converging and squeezing flows that occur in typical polymer processing operations.
  • Extensional melt flow measurements are particularly useful in polymer characterization because they are very sensitive to the molecular structure of the polymeric system being tested.
  • the true strain rate of extension also referred to as the Hencky strain rate
  • simple extension is said to be a "strong flow” in the sense that it can generate a much higher degree of molecular orientation and stretching than flows in simple shear.
  • extensional flows are very sensitive to crystallinity and macro-structural effects, such as long-chain branching, and as such can be far more descriptive with regard to polymer characterization than other types of bulk rheological measurement which apply shear flow.
  • the multi-branching index is defined as the slope of the strain hardening index (SHI) as a function of Ig ⁇ d ⁇ /dt) [d SHI/d Ig ⁇ d ⁇ /dt)].
  • the inventive blown film and/or the polypropylene of said film is (are) preferably characterized by the fact that their strain hardening index (SHI) increases with the deformation rate ⁇ H , i.e. a phenomenon which is not observed in other polypropylenes.
  • strain hardening index (SHI) is not influenced by the deformation rate (see Figures 2 and 3). Accordingly, the strain hardening index (SHI) of known polymers, in particular known polypropylenes and polyethylenes, does not increase or increases only negligible with increase of the deformation rate (d ⁇ /dt).
  • strain hardening index (SHI@l s " ') of the blown film and/or the polypropylene of said film shall be at least 0.30, more preferred of at least 0.40, still more preferred of at least 0.50.
  • the strain hardening index (SHI) is a measure for the strain hardening behavior of the polymer melt, in particular of the polypropylene melt.
  • the strain hardening index (SHI@l s " ') has been measured by a deformation rate (d ⁇ /dt) of 1.00 s "1 at a temperature of 180 °C for determining the strain hardening behavior, wherein the strain hardening index (SHI) is defined as the slope of the tensile stress growth function ⁇ + as a function of the Hencky strain f on a logarithmic scale between 1.00 and 3.00 (see figure 1 ).
  • the Hencky strain rate ⁇ H is defined by the formula
  • L 0 is the fixed, unsupported length of the specimen sample being stretched which is equal to the centerline distance between the master and slave drums
  • R is the radius of the equi-dimensional windup drums
  • the branching index g' of the inventive polypropylene of the blown film shall be less than 1.00, more preferably less than 0.90, still more preferably less than 0.80.
  • the branching index g 1 shall be less than 0.75, i.e. 0.70 or less.
  • the branching index g' is more than 0.6, still more preferably 0.7 or more.
  • the branching index g' of the polypropylene is in the range of 0.6 to below 1.0, more preferred in the range of more than 0.65 to 0.95, still more preferred in the range of 0.7 to 0.95.
  • the branching index g' defines the degree of branching and correlates with the amount of branches of a polymer.
  • a low g'- value is an indicator for a high branched polymer. In other words, if the g'- value decreases, the branching of the polypropylene increases.
  • the branching index g' is preferably of less than 1.00, more preferably less than 0.90, still more preferably less than 0.80. In the preferred embodiment, the branching index g' of the blown film shall be less than 0.75, i.e. 0.7 or less.
  • the intrinsic viscosity needed for determining the branching index g 1 is measured according to DIN ISO 1628/1 , October 1999 (in Decalin at 135 0 C).
  • the inventive blown film and/or the polypropylene of said film has (have) a branching index g' of less than 1.00, a strain hardening index (SHI@ls " ') of at least 0.30 and multi-branching index (MBI) of at least 0.15. Still more preferred the inventive blown film and/or the polypropylene of said film has (have) a branching index g' of less than 0.80, a strain hardening index (SHI@l s " ') of at least 0.40 and multi- branching index (MBI) of at least 0.15.
  • inventive blown film and/or the polypropylene of said film has (have) a branching index g' of less than 1.00, a strain hardening index (SHI@l s " ') of at least 0.30 and multi-branching index (MBI) of at least 020.
  • inventive blown film and/or the polypropylene of said film has (have) a branching index g' of less than 0.80, a strain hardening index (SHI@l s " ') of at least 0.40 and multi-branching index (MBI) of at least 020.
  • inventive blown film and/or the polypropylene of said film has (have) a branching index g' of less than 0.80, a strain hardening index (SHI@l s " ') of at least 0.50 and multi-branching index (MBI) of at least 030.
  • the blown film according to the third embodiment is free of polyethylene, even more preferred the blown film comprises a polypropylene as defined above and further defined below as the only polymer component.
  • the further features mentioned below apply to all embodiments described above, i.e. the first, the second and the third embodiment as defined above.
  • the polypropylene used for the blown film shall be not cross-linked as it is commonly done to improve the process properties of the polypropylene.
  • the cross-linking is detrimental in many aspects. Inter alia the manufacture of said products is difficult to obtain.
  • blown film according to the instant invention is further characterized in that the blown film has only gels with a diameter of equal or less than 500 ⁇ m, i.e. no gels with a diameter of more than 500 ⁇ m are present in said film, and wherein said gels are not more than 100 gels per square meter (sqm), more preferably not more than 80 gels per square meter (sqm), and yet more preferably not more than 60 gels per square meter (sqm).
  • the blown film has only gels with a diameter of equal or less than 400 ⁇ m, i.e.
  • the blown film has only gels with a diameter of equal or less than 300 ⁇ m, i.e.
  • no gels with a diameter of more than 500 ⁇ m are present in said film, and wherein said gels are not more than 100 gels per square meter (sqm), more preferably not more than 80 gels per square meter (sqm), and yet more preferably not more than 60 gels per square meter (sqm).
  • the polypropylene has a melt flow rate (MFR) given in a specific range.
  • MFR melt flow rate
  • the melt flow rate mainly depends on the average molecular weight. This is due to the fact that long molecules render the material a lower flow tendency than short molecules. An increase in molecular weight means a decrease in the MFR-value.
  • the melt flow rate (MFR) is measured in g/10 min of the polymer discharged through a defined dye under specified temperature and pressure conditions and the measure of viscosity of the polymer which, in turn, for each type of polymer is mainly influenced by its molecular weight but also by its degree of branching.
  • the melt flow rate measured under a load of 2.16 kg at 230 °C (ISO 1 133) is denoted as MFR 2 .
  • the polypropylene has an MFR 2 in a range of 0.01 to 1000.00 g/10 min, more preferably of 0.01 to 100.00 g/10 min, still more preferred of 0.05 to 50 g/10 min.
  • the MFR is in a range of 1 .00 to 1 1.00 g/10 min.
  • the MFR is in a range of 3.00 to 1 1.00 g/10 min.
  • the number average molecular weight (Mn) is an average molecular weight of a polymer expressed as the first moment of a plot of the number of molecules in each molecular weight range against the molecular weight. In effect, this is the total molecular weight of all molecules divided by the number of molecules.
  • the weight average molecular weight (Mw) is the first moment of a plot of the weight of polymer in each molecular weight range against molecular weight.
  • the number average molecular weight (Mn) and the weight average molecular weight (Mw) as well as the molecular weight distribution are determined by size exclusion chromatography (SEC) using Waters Alliance GPCV 2000 instrument with online viscometer.
  • the oven temperature is 140 °C.
  • Trichlorobenzene is used as a solvent.
  • the polypropylene has a weight average molecular weight (Mw) from 10,000 to 2,000,000 g/mol, more preferably from 20,000 to 1 ,500,000 g/mol. More preferably, the polypropylene of the instant invention is isotactic.
  • Mw weight average molecular weight
  • the polypropylene according to this invention shall have a rather high pentade concentration, i.e. higher than 90 %, more preferably higher than 92 % and most preferably higher than 93 %. In another preferred embodiment the pentade concentration is higher than 95 %.
  • the pentade concentration is an indicator for the narrowness in the stereoregularity distribution of the polypropylene.
  • the polypropylene has a melting temperature Tm of higher than 120 °C. It is in particular preferred that the melting temperature is higher than 120 °C if the polypropylene is a polypropylene copolymer as defined below. In turn, in case the polypropylene is a polypropylene homopolymer as defined below, it is preferred, that polypropylene has a melting temperature of higher than 140 °C, more preferred higher than 145 °C.
  • the blown film has a melting temperature Tm of higher than 120 °C. It is in particular preferred that the melting temperature of the blown film is higher than 120 °C, more preferably higher than 130 °C, and yet more preferred higher than 135 °C, in case the polypropylene is a propylene copolymer as defined in the present invention. In turn the polypropylene is a propylene homopolymer as defined in the present invention, it is preferred that the melting temperature of the blown film is higher than 140 °C, more preferably higher than 150 °C, and yet more preferably higher than 155 °C.
  • the amount of solubles of the blown film shall be rather low. Accordingly the amount of xylene solubles of the blown film shall be preferably less than 2.00 wt.-%, more preferably less than 1.00 wt.-% and still more preferably less than 0.80 wt.-%.
  • Xylene solubles are the part of the polymer soluble in cold xylene determined by dissolution in boiling xylene and letting the insoluble part crystallize from the cooling solution (for the method see below in the experimental part).
  • the xylene solubles fraction contains polymer chains of low stereo-regularity and is an indication for the amount of non-crystalline areas.
  • polypropylene as defined above is preferably unimodal. In another preferred embodiment the polypropylene as defined above (and further defined below) is preferably multimodal, more preferably bimodal.
  • Multimodal or “multimodal distribution” describes a frequency distribution that has several relative maxima.
  • the expression “modality of a polymer” refers to the form of its molecular weight distribution (MWD) curve, i.e. the appearance of the graph of the polymer weight fraction as a function of its molecular weight. If the polymer is produced in the sequential step process, i.e. by utilizing reactors coupled in series, and using different conditions in each reactor, the different polymer fractions produced in the different reactors each have their own molecular weight distribution which may considerably differ from one another.
  • the molecular weight distribution curve of the resulting final polymer can be seen at a super-imposing of the molecular weight distribution curves of the polymer fraction which will, accordingly, show a more distinct maxima, or at least be distinctively broadened compared with the curves for individual fractions.
  • a polymer showing such molecular weight distribution curve is called bimodal or multimodal, respectively.
  • the polypropylene of the blown film is not unimodal it is preferably bimodal.
  • the polypropylene according to this invention can be homopolymer or a copolymer. Accordingly, the homopolymer as well as the copolymer can be a multimodal polymer composition.
  • the expression homopolymer used herein relates to a polypropylene that consists substantially, i.e. of at least 97 wt%, preferably of at least 99 wt%, and most preferably of at least 99.8 wt% of propylene units. In a preferred embodiment only propylene units in the polypropylene homopolymer are detectable.
  • the comonomer content can be determined with FT infrared spectroscopy, as described below in the examples.
  • the polypropylene used for the preparation of the blown film is a propylene copolymer
  • the comonomer is ethylene.
  • the total amount of comonomer, more preferably ethylene, in the propylene copolymer is up to 10 mol%, more preferably up to 8 mol%, and even more preferably up to 6 mol%.
  • the polypropylene is a propylene copolymer comprising a polypropylene matrix and an ethylene-propylene rubber (EPR).
  • EPR ethylene-propylene rubber
  • the polypropylene matrix can be a homopolymer or a copolymer, more preferably multimodal, i.e. bimodal, homopolymer or a multimodal, i.e. bimodal, copolymer.
  • the polypropylene matrix is a propylene copolymer
  • the comonomer is ethylene or butene.
  • the preferred amount of comonomer, more preferably ethylene, in the polypropylene matrix is up to 8.00 Mol%.
  • the propylene copolymer matrix has ethylene as the comonomer component, it is in particular preferred that the amount of ethylene in the matrix is up to 8.00 Mol%, more preferably less than 6.00 Mol%. In case the propylene copolymer matrix has butene as the comonomer component, it is in particular preferred that the amount of butene in the matrix is up to 6.00 Mol%, more preferably less than 4.00 Mol%.
  • the ethylene-propylene rubber (EPR) in the total propylene copolymer is less than or equal 50 wt%, more preferably less than or equal 40 wt%. Yet more preferably the amount of ethylene-propylene rubber (EPR) in the total propylene copolymer is in the range of 10 to 50 wt%, still more preferably in the range of 10 to 40 wt%.
  • the polypropylene being a copolymer comprising a polypropylene matrix and an ethylene-propylene rubber (EPR) has an ethylene-propylene rubber (EPR) with an ethylene-content of up to 50 wt%.
  • the polypropylene as defined above is produced in the presence of the catalyst as defined below. Furthermore, for the production of the polypropylene of the inventive blown film as defined above, the process as stated below is preferably used.
  • a metallocene catalyst is used for the polypropylene of the coated extrusion film.
  • the polypropylene according to this invention is obtainable by a new catalyst system.
  • This new catalyst system comprises an asymmetric catalyst, whereby the catalyst system has a porosity of less than 1.40 ml/g, more preferably less than 1.30 ml/g and most preferably less than 1.00 ml/g.
  • the porosity has been measured according to DIN 66135 (N 2 ).
  • the porosity is not detectable when determined with the method applied according to DIN 66135 (N 2 ).
  • An asymmetric catalyst according to this invention is a metallocene compound comprising at least two organic ligands which differ in their chemical structure. More preferably the asymmetric catalyst according to this invention is a metallocene compound comprising at least two organic ligands which differ in their chemical structure and the metallocene compound is free of C 2 - symmetry and/or any higher symmetry.
  • the asymetric metallocene compound comprises only two different organic ligands, still more preferably comprises only two organic ligands which are different and linked via a bridge.
  • Said asymmetric catalyst is preferably a single site catalyst (SSC).
  • SSC single site catalyst
  • the catalyst system has a surface area of less than 25 m 2 /g, yet more preferred less than 20 mVg, still more preferred less than 15 m 2 /g, yet still less than 10 mVg and most preferred less than 5 mVg.
  • the surface area according to this invention is measured according to ISO 9277 (N 2 ).
  • the catalytic system according to this invention comprises an asymmetric catalyst, i.e. a catalyst as defined below, and has porosity not detectable when applying the method according to DIN 66135 (N 2 ) and has a surface area measured according to ISO 9277 (N 2 ) less than 5 mVg.
  • the asymmetric catalyst compound i.e. the asymetric metallocene, has the formula (I):
  • M is Zr, Hf or Ti, more preferably Zr, and X is independently a monovalent anionic ligand, such as ⁇ -ligand
  • R is a bridging group linking the two Cp ligands
  • Cp is an organic ligand selected from the group consisting of unsubstituted cyclopenadienyl, unsubstituted indenyl, unsubstituted tetrahydroindenyl, unsubstituted fluorenyl, substituted cyclopenadienyl, substituted indenyl, substituted tetrahydroindenyl, and substituted fluorenyl, with the proviso that both Cp-ligands are selected from the above stated group and both Cp-ligands have a different chemical structure.
  • ⁇ -ligand is understood in the whole description in a known manner, i.e. a group bonded to the metal at one or more places via a sigma bond.
  • a preferred monovalent anionic ligand is halogen, in particular chlorine (Cl).
  • the asymmetric catalyst is of formula (I) indicated above, wherein M is Zr and each X is Cl.
  • both identical Cp-ligands are substituted.
  • both Cp-ligands have different residues to obtain an asymmetric structure.
  • both Cp-ligands are selected from the group consisting of substituted cyclopenadienyl-ring, substituted indenyl-ring, substituted tetrahydroindenyl-ring, and substituted fluorenyl-ring wherein the Cp-ligands differ in the substituents bonded to the rings.
  • the optional one or more substituent(s) bonded to cyclopenadienyl, indenyl, tetrahydroindenyl, or fluorenyl may be independently selected from a group including halogen, hydrocarbyl (e.g.
  • Ci-C 20 -alkyl C 2 -C 20 -alkenyl, C 2 -C 20 - alkynyl, C 3 -Ci 2 -cycloalkyl, C 6 -C 20 -aryl or C 7 -C 20 -arylalkyl), C 3 -C) 2 -cycloalkyl which contains 1 , 2, 3 or 4 heteroatom(s) in the ring moiety, C 6 -C 20 - heteroaryl, C,-C 20 -haloalkyl, -SiR" 3 , -OSiR" 3 , -SR", -PR" 2 and -NR" 2 , wherein each R" is independently a hydrogen or hydrocarbyl, e.g.
  • both Cp-ligands are indenyl moieties wherein each indenyl moiety bear one or two substituents as defined above. More preferably each Cp-ligand is an indenyl moiety bearing two substituents as defined above, with the proviso that the substituents are chosen in such are manner that both Cp- ligands are of different chemical structure, i.e both Cp-ligands differ at least in one substituent bonded to the indenyl moiety, in particular differ in the substituent bonded to the five member ring of the indenyl moiety.
  • both Cp are indenyl moieties wherein the indenyl moieties comprise at least at the five membered ring of the indenyl moiety, more preferably at 2-position, a substituent selected from the group consisting of alkyl, such as Ci-C 6 alkyl, e.g. methyl, ethyl, isopropyl, and trialkyloxysiloxy, wherein each alkyl is independently selected from Ci-C 6 alkyl, such as methyl or ethyl, with proviso that the indenyl moieties of both Cp must chemically differ from each other, i.e. the indenyl moieties of both Cp comprise different substituents.
  • alkyl such as Ci-C 6 alkyl, e.g. methyl, ethyl, isopropyl, and trialkyloxysiloxy
  • each alkyl is independently selected from Ci-C 6 alkyl, such as methyl or ethyl, with provis
  • both Cp are indenyl moieties wherein the indenyl moieties comprise at least at the six membered ring of the indenyl moiety, more preferably at 4-position, a substituent selected from the group consisting of a C 6 -C 20 aromatic ring moiety, such as phenyl or naphthyl, preferably phenyl, which is optionally substituted with one or more substitutents, such as Ci-C 6 alkyl, and a heteroaromatic ring moiety, with proviso that the indenyl moieties of both Cp must chemically differ from each other, i.e. the indenyl moieties of both Cp comprise different substituents.
  • both Cp are indenyl moieties wherein the indenyl moieties comprise at the five membered ring of the indenyl moiety, more preferably at 2-position, a substituent and at the six membered ring of the indenyl moiety, more preferably at 4-position, a further substituent, wherein the substituent of the five membered ring is selected from the group consisting of alkyl, such as Cj-C 6 alkyl, e.g.
  • each alkyl is independently selected from Ci-C 6 alkyl, such as methyl or ethyl
  • the further substituent of the six membered ring is selected from the group consisting of a C 6 -C 20 aromatic ring moiety, such as phenyl or naphthyl, preferably phenyl, which is optionally substituted with one or more substituents, such as Ci-C 6 alkyl, and a heteroaromatic ring moiety, with proviso that the indenyl moieties of both Cp must chemically differ from each other, i.e. the indenyl moieties of both Cp comprise different substituents.
  • both Cp are idenyl rings comprising two substituentes each and differ in the substituents bonded to the five membered ring of the idenyl rings.
  • Y is C, Si or Ge
  • R' is Ci to C 20 alkyl, C 6 -C] 2 aryl, or C 7 -Ci 2 arylalkyl or trimethylsilyl.
  • the bridge member R is typically placed at 1 -position.
  • the bridge member R may contain one or more bridge atoms selected from e.g. C, Si and/or Ge, preferably from C and/or Si.
  • One preferable bridge R is -Si(R') 2 -, wherein R' is selected independently from one or more of e.g.
  • Ci-C] 0 alkyl Ci-C 20 alkyl, such as C 6 -Ci 2 aryl, or C 7 -C 40 , such as C 7 -Ci 2 arylalkyl, wherein alkyl as such or as part of arylalkyl is preferably Ci-C 6 alkyl, such as ethyl or methyl, preferably methyl, and aryl is preferably phenyl.
  • the bridge -Si(R')2- is preferably e.g.
  • the asymmetric catalyst i.e. the asymetric metallocene, is defined by the formula (III)
  • Cp Cp 2 R 1 ZrCl 2 (III) wherein both Cp coordinate to M and are selected from the group consisting of unsubstituted cyclopenadienyl, unsubstituted indenyl, unsubstituted tetrahydroindenyl, unsubstituted fluorenyl, substituted cyclopenadienyl, substituted indenyl, substituted tetrahydroindenyl, and substituted fluorenyl, with the proviso that both Cp-ligands are of different chemical structure, and
  • R is a bridging group linking two ligands L, wherein R is defined by the formula (II) -Y(R') 2 - (II) wherein
  • Y is C, Si or Ge
  • R' is Ci to C 20 alkyl, C 6 -Ci 2 aryl, or C 7 -Ci 2 arylalkyl.
  • the asymmetric catalyst is defined by the formula (III), wherein both Cp are selected from the group consisting of substituted cyclopenadienyl, substituted indenyl, substituted tetrahydroindenyl, and substituted fluorenyl.
  • the asymmetric catalyst is defined by the formula (III), wherein both Cp are selected from the group consisting of substituted cyclopenadienyl, substituted indenyl, substituted tetrahydroindenyl, and substituted fluorenyl with the proviso that both Cp-ligands differ in the substituents, i.e. the subtituents as defined above, bonded to cyclopenadienyl, indenyl, tetrahydroindenyl, or fluorenyl.
  • the asymmetric catalyst is defined by the formula (III), wherein both Cp are indenyl and both indenyl differ in one substituent, i.e. in a substiuent as defined above bonded to the five member ring of indenyl.
  • the asymmetric catalyst is a non-silica supported catalyst as defined above, in particular a metallocene catalyst as defined above.
  • the asymmetric catalyst is dimethylsilyl [(2- methyl-(4'-tert.butyl)-4-phenyl-indenyl)(2-isopropyl-(4'-tert.butyl)-4-phenyl- indenyl)]zirkonium dichloride (IUPAC: dimethylsilandiyl [(2-methyl-(4'- tert.butyl)-4-phenyl-indenyl)(2-isopropyl-(4'-tert.butyl)-4-phenyl- indenyl)]zirkonium dichloride). More preferred said asymmetric catalyst is not silica supported.
  • the asymmetric catalyst system is obtained by the emulsion solidification technology as described in WO 03/051934.
  • the asymmetric catalyst is preferably in the form of solid catalyst particles, obtainable by a process comprising the steps of a) preparing a solution of one or more asymmetric catalyst components; b) dispersing said solution in a solvent immiscible therewith to form an emulsion in which said one or more catalyst components are present in the droplets of the dispersed phase, c) solidifying said dispersed phase to convert said droplets to solid particles and optionally recovering said particles to obtain said catalyst.
  • a solvent more preferably an organic solvent, is used to form said solution.
  • the organic solvent is selected from the group consisting of a linear alkane, cyclic alkane, linear alkene, cyclic alkene, aromatic hydrocarbon and halogen-containing hydrocarbon.
  • the immiscible solvent forming the continuous phase is an inert solvent, more preferably the immiscible solvent comprises a fluorinated organic solvent and/or a functionalized derivative thereof, still more preferably the immiscible solvent comprises a semi-, highly- or perfluorinated hydrocarbon and/or a functionalized derivative thereof.
  • said immiscible solvent comprises a perfluorohydrocarbon or a f ⁇ inctionalized derivative thereof, preferably C 3 -C 30 perfluoroalkanes, -alkenes or - cycloalkanes, more preferred C 4 -Ci 0 perfluoro-alkanes, -alkenes or -cycloalkanes, particularly preferred perfluorohexane, perfluoroheptane, perfluorooctane or perfluoro (methylcyclohexane) or a mixture thereof.
  • a perfluorohydrocarbon or a f ⁇ inctionalized derivative thereof preferably C 3 -C 30 perfluoroalkanes, -alkenes or - cycloalkanes, more preferred C 4 -Ci 0 perfluoro-alkanes, -alkenes or -cycloalkanes, particularly preferred perfluorohexane, per
  • the emulsion comprising said continuous phase and said dispersed phase is a bi-or multiphasic system as known in the art.
  • An emulsifier may be used for forming the emulsion. After the formation of the emulsion system, said catalyst is formed in situ from catalyst components in said solution.
  • the emulsifying agent may be any suitable agent which contributes to the formation and/or stabilization of the emulsion and which does not have any adverse effect on the catalytic activity of the catalyst.
  • the emulsifying agent may e.g. be a surfactant based on hydrocarbons optionally interrupted with (a) heteroatom(s), preferably halogenated hydrocarbons optionally having a functional group, preferably semi-, highly- or perfluorinated hydrocarbons as known in the art.
  • the emulsifying agent may be prepared during the emulsion preparation, e.g. by reacting a surfactant precursor with a compound of the catalyst solution.
  • Said surfactant precursor may be a halogenated hydrocarbon with at least one functional group, e.g. a highly fluorinated Ci to C 30 alcohol, which reacts e.g. with a cocatalyst component, such as aluminoxane.
  • a halogenated hydrocarbon with at least one functional group e.g. a highly fluorinated Ci to C 30 alcohol, which reacts e.g. with a cocatalyst component, such as aluminoxane.
  • any solidification method can be used for forming the solid particles from the dispersed droplets.
  • the solidification is effected by a temperature change treatment.
  • the emulsion subjected to gradual temperature change of up to 10 °C/min, preferably 0.5 to 6 °C/min and more preferably 1 to 5 °C/min.
  • the emulsion is subjected to a temperature change of more than 40 °C, preferably more than 50 °C within less than 10 seconds, preferably less than 6 seconds.
  • the recovered particles have preferably an average size range of 5 to 200 ⁇ m, more preferably 10 to 100 ⁇ m.
  • the form of solidified particles have preferably a spherical shape, a predetermined particles size distribution and a surface area as mentioned above of preferably less than 25 m /g, still more preferably less than 20 m /g, yet more preferably less than 15 m 2 /g, yet still more preferably less than 10 m 2 /g and most preferably less than 5 m 2 /g, wherein said particles are obtained by the process as described above.
  • the catalyst system may further comprise an activator as a cocatalyst, as described in WO 03/051934, which is enclosed herein with reference.
  • cocatalysts for metallocenes and non-metallocenes are the aluminoxanes, in particular the Ci-Ci 0 -alkylaluminoxanes, most particularly methylaluminoxane (MAO).
  • aluminoxanes can be used as the sole cocatalyst or together with other cocatalyst(s).
  • other cation complex forming catalysts activators can be used. Said activators are commercially available or can be prepared according to the prior art literature. Further aluminoxane cocatalysts are described i.a.
  • ratio of the transition metal to boron activator may be used.
  • aluminoxanes such as methylaluminumoxane (MAO)
  • MAO methylaluminumoxane
  • the amount of Al, provided by aluminoxane can be chosen to provide a molar ratio of Al transition metal e.g. in the range of 1 to 10 000, suitably 5 to 8000, preferably 10 to 7000, e.g. 100 to 4000, such as 1000 to 3000.
  • the ratio is preferably below 500.
  • the quantity of cocatalyst to be employed in the catalyst of the invention is thus variable, and depends on the conditions and the particular transition metal compound chosen in a manner well known to a person skilled in the art.
  • any additional components to be contained in the solution comprising the organotransition compound may be added to said solution before or, alternatively, after the dispersing step.
  • the present invention is related to the use of the above-defined catalyst system for the production of polymers, in particular of a polypropylene according to this invention.
  • the present invention is related to the process for producing the inventive polypropylene, whereby the catalyst system as defined above is employed. Furthermore it is preferred that the process temperature is higher than 60 0 C. Preferably, the process is a multi-stage process to obtain multimodal polypropylene as defined above.
  • Multistage processes include also bulk/gas phase reactors known as multizone gas phase reactors for producing multimodal propylene polymer.
  • a preferred multistage process is a "loop-gas phase"-process, such as developed by Borealis A/S, Denmark (known as BORSTAR® technology) described e.g. in patent literature, such as in EP 0 887 379 or in WO 92/12182.
  • Multimodal polymers can be produced according to several processes which are described, e.g. in WO 92/12182, EP 0 887 379 and WO 97/22633.
  • a multimodal polypropylene according to this invention is produced preferably in a multi-stage process in a multi-stage reaction sequence as described in WO 92/12182. The contents of this document are included herein by reference.
  • the main polymerization stages are preferably carried out as a combination of a bulk polymerization/gas phase polymerization.
  • the bulk polymerizations are preferably performed in a so-called loop reactor.
  • the composition be produced in two main polymerization stages in combination of loop reactor/gas phase reactor.
  • the process may also comprise a prepolymerization step in a manner known in the field and which may precede the polymerization step (a).
  • a further elastomeric comonomer component so called ethylene- propylene rubber (EPR) component as defined in this invention, may be incorporated into the obtained propylene polymer to form a propylene copolymer as defined above.
  • the ethylene-propylene rubber (EPR) component may preferably be produced after the gas phase polymerization step (b) in a subsequent second or further gas phase polymerizations using one or more gas phase reactors.
  • the process is preferably a continuous process.
  • the conditions for the bulk reactor of step (a) may be as follows:
  • the temperature is within the range of 40 0 C to 1 10 °C, preferably between 60 °C and 100 °C, 70 to 90 °C
  • the pressure is within the range of 20 bar to 80 bar, preferably between 30 bar to 60 bar
  • - hydrogen can be added for controlling the molar mass in a manner known per se.
  • step (b) the reaction mixture from the bulk (bulk) reactor (step a) is transferred to the gas phase reactor, i.e. to step (b), whereby the conditions in step (b) are preferably as follows: the temperature is within the range of 50 °C to 130 °C, preferably between 60 °C and 100 °C, the pressure is within the range of 5 bar to 50 bar, preferably between 15 bar to 35 bar, hydrogen can be added for controlling the molar mass in a manner known per se.
  • the residence time can vary in both reactor zones.
  • the residence time in bulk reactor, e.g. loop is in the range 0.5 to 5 hours, e.g. 0.5 to 2 hours and the residence time in gas phase reactor will generally be 1 to 8 hours.
  • the polymerization may be effected in a known manner under supercritical conditions in the bulk, preferably loop reactor, and/or as a condensed mode in the gas phase reactor.
  • the process of the invention or any embodiments thereof above enable highly feasible means for producing and further tailoring the propylene polymer composition within the invention, e.g. the properties of the polymer composition can be adjusted or controlled in a known manner e.g. with one or more of the following process parameters: temperature, hydrogen feed, comonomer feed, propylene feed e.g. in the gas phase reactor, catalyst, the type and amount of an external donor (if used), split between components.
  • More over the present invention is related to the manufacture of the inventive blown film by extrusion of the polypropylene as defined herein by conventional blown film extrusion, i.e. the polypropylene is extruded through a die, preferably circular die, followed by "bubble-like" expansion.
  • the blown films according to this invention are preferably produced on a single screw extruder with a barrel diameter of 70 mm and a round-section die of 200 mm with 1 mm die gap in combination with a monolip cooling ring and internal bubble cooling (IBC).
  • Melt temperature is preferably 210 °C in the die; the temperature of the cooling air is kept preferably at 15 °C and the blow up ratio (BUR) is preferably 3:1.
  • BUR blow up ratio
  • a film thickness of 40 ⁇ m is adjusted through the ratio between extruder output, takeoff speed and BUR.
  • the present invention is also directed to the use of the inventive blown film, as packaging material, in particular as a packaging material for food and/or medical products.
  • the present invention is related to articles comprising a blown film as defined herein and/or a polypropylene as defined herein.
  • the present invention is directed to the use of the inventive polypropylene as defined herein for blown films and/or articles comprising at least said blown films.
  • Possible articles for which the inventive blown film and/or the inventive polypropylene can be used are lamination films, general packaging films, like bread bags, pouches and medical/hygienic films.
  • pentad concentration analysis For the meso pentad concentration analysis, also referred herein as pentad concentration analysis, the assignment analysis is undertaken according to T Hayashi, Pentad concentration, R. Chujo and T. Asakura, Polymer 29 138-43 (1988) and Chujo R, et al., Polymer 35 339 (1994)
  • a Paar Physica MCR300 equipped with a TC30 temperature control unit and an oven CTT600 (convection and radiation heating) and a SERVPO 1-025 extensional device with temperature sensor and a software RHEOPLUS/32 v2.66 is used.
  • the device is set to test temperature (180°C) for minimum 20minutes without sample in presence of the clamps
  • the torque (measured in mNm) is recorded and plotted against time •
  • the torque must not exceed a value of 5x10-3 mNm to make sure that the friction of the device is in an acceptably low range
  • the device is heated for min. 20min to the test temperature (180°C measured with the thermocouple attached to the SER device) with clamps but without sample. Subsequently, the sample (0.7x1 Ox 18mm), prepared as described above, is clamped into the hot device. The sample is allowed to melt for 2 minutes +/- 20 seconds before the experiment is started.
  • the device After stretching, the device is opened and the stretched film (which is winded on the drums) is inspected. Homogenous extension is required. It can be judged visually from the shape of the stretched film on the drums if the sample stretching has been homogenous or not.
  • the tape must me wound up symmetrically on both drums, but also symmetrically in the upper and lower half of the specimen.
  • the transient elongational viscosity calculates from the recorded torque as outlined below.
  • the resulting tensile stress growth function ⁇ e + (d ⁇ /dt, t) is plotted against the total Hencky strain ⁇ to determine the strain hardening behaviour of the melt, see Figure 1.
  • E + can be well fitted with a function
  • strain rate short chain-, hyper- or multi-branched structures
  • HDPE linear
  • LLDPE short-chain branched
  • LDPE hyperbranched structures
  • the first polymer is a H- and Y-shaped polypropylene homopolymer made according to EP 879 830 ("A") example 1 through adjusting the MFR with the amount of butadiene. It has a MFR230/2.16 of 2.0g/10min, a tensile modulus of 1950MPa and a branching index g' of 0.7.
  • the second polymer is a commercial hyperbranched LDPE, Borealis "B", made in a high pressure process known in the art. It has a MFR190/2.16 of 4.5 and a density of 923kg/m 3 .
  • the third polymer is a short chain branched LLDPE, Borealis "C", made in a low pressure process known in the art. It has a MFRl 90/2.16 of 1.2 and a density of 919kg/m ⁇
  • the fourth polymer is a linear HDPE, Borealis "D", made in a low pressure process known in the art. It has a MFRl 90/2.16 of 4.0 and a density of 954kg/m 3 .
  • the four materials of known chain architecture are investigated by means of measurement of the transient elongational viscosity at 180°C at strain rates of 0.10, 0.30, 1.0, 3.0 and 10s "1 . Obtained data (transient elongational viscosity versus Hencky strain) is fitted with a function
  • the parameters cl and c2 are found through plotting the logarithm of the transient elongational viscosity against the logarithm of the Hencky strain and performing a linear fit of this data applying the least square method.
  • the parameter cl calculates from the intercept of the linear fit of the data lg ⁇ + ) versus lg( ⁇ ) from
  • C i 1 0 lntercept and C 2 is the strain hardening index (SHl) at the particular strain rate.
  • a multi- branching index is calculated from the slope of a linear fitting curve of SHI versus ⁇ g( ⁇ H ):
  • the multi-branching index MBI allows now to distinguish between Y or H- branched polymers which show a MBI smaller than 0.05 and hyper-branched polymers which show a MBI larger than 0.15. Further, it allows to distinguish between short-chain branched polymers with MBI larger than 0.10 and linear materials which have a MBI smaller than 0.10.
  • strain hardening index SHI
  • MBI multi-branching index
  • Particle size distribution is measured via Coulter Counter LS 200 at room temperature with n-heptane as medium.
  • the NMR-measurement was used for determining the mmmm pentad concentration in a manner well known in the art.
  • M n Number average molecular weight
  • M w weight average molecular weight
  • MFD molecular weight distribution
  • SEC size exclusion chromatography
  • the oven temperature is 140 °C.
  • Trichlorobenzene is used as a solvent (ISO 16014).
  • the number average molecular weight (M n ), the weight average molecular weight (M w ) and the molecular weight distribution (MWD) are measured by a method based on ISO 16014-1 :2003 and ISO 16014-4:2003.
  • sample solution 216.5 ⁇ L were injected per analysis.
  • the column set was calibrated using relative calibration with 19 narrow MWD polystyrene (PS) standards in the range of 0.5 kg/mol to 1 1 500 kg/mol and a set of well characterized broad polypropylene standards. All samples were prepared by dissolving 5 - 10 mg of polymer in 10 mL (at 160 °C) of stabilized TCB (same as mobile phase) and keeping for 3 hours with continuous shaking prior sampling in into the GPC instrument.
  • PS polystyrene
  • the xylene solubles (XS, wt.-%): Analysis according to the known method: 2.0 g of polymer is dissolved in 250 ml p-xylene at 135°C under agitation. After 30 ⁇ 2 minutes the solution is allowed to cool for 15 minutes at ambient temperature and then allowed to settle for 30 minutes at 25 ⁇ 0.5°C. The solution is filtered and evaporated in nitrogen flow and the residue dried under vacuum at 90 °C until constant weight is reached.
  • melt- and crystallization enthalpy were measured by the DSC method according to ISO 1 1357-3.
  • the method determines the sealing temperature range of polypropylene films, in particular blown films.
  • the sealing temperature range is the temperature range, in which the films can be sealed according to conditions given below.
  • the lower limit heat sealing initiation temperature (SIT)
  • SIT heat sealing initiation temperature
  • SET ling end temperature
  • sample geometry and sample preparation The samples are extruded with OCS at 220 °C and taken in longitudinal direction of extrusion.
  • the sample size is 45 mm x 170 mm, the film thickness is 50 ⁇ m.
  • Sealing Device For sealing the laboratory sealing device KOPP SGPE-20 is used. Prior to the test, the device is checked for the parallel position of the sealing jaws.
  • the sealing parameters are set to: Sealing force: 600 N
  • Sealing jaws 100 x 20 mm, smooth
  • Stripes are folded to 85 x 45 mm and put between the sealing jaws. The jaws are heated to sealing temperature Immediately after sealing, the sample is taken out of the device - For each temperature, 10 samples are sealed
  • the heat sealing initiation temperature SIT
  • the sealing temperature is increased by 2 °C and the test is repeated. After having reached the heat sealing initiation temperature (SIT), the sealing temperature is further increased in steps of 2 °C until the film sticks to the sealing jaws.
  • the heat sealing initiation temperature is the temperature where a sealing strength of > 5 N is reached.
  • the sealing end temperature is the temperature where the film sticks to the sealing jaws.
  • the precision of the method is determined by the temperature steps, i.e. 2 °C.
  • MFR 2 measured according to ISO 1 133 (230°C, 2.16 kg load).
  • Comonomer content is measured with Fourier transform infrared spectroscopy (FTIR) calibrated with 13 C-NMR.
  • FTIR Fourier transform infrared spectroscopy
  • Stiffness Film TD transversal direction
  • Stiffness Film MD machine direction
  • Elongation at break TD Elongation at break MD: these are determined according to ISO 527-3 (cross head speed: 1 mm/min).
  • Stiffness (tensile modulus) of the injection molded samples (states) is measured according to ISO 527-2. The modulus is measured at a speed of 1 mm/min.
  • Haze and transparency are determined according to ASTM Dl 003-92 (haze).
  • GeIs Gels are determined by visual counting using the following equipment.
  • the OCS equipment is used for continuous gel determination (counting, classification and documentation) in PP films.
  • the equipment is assembled by the following components: Extruder: Lab extruder ME25/5200, 3 heating zones (up to 450 0 C) Screw diameter 25, LfD 25
  • Intrinsic viscosity is measured according to DIN ISO 1628/1 , October 1999 (in Decalin at 135 0 C).
  • a commercial linear Z/N Polypropylene copolymer with ethylene has an MFR 23 o/ 2 i 6 of 1.9g/10min, a g' of 1.0, an ethylene content of 6.5 mol % and a fraction of xylene soulubles of 7.8 wt %.
  • the material is made with the Borstar process known in the art. It has a melting temperature of 138 0 C and a melt enthalpy of 75 J/g.
  • a support-free catalyst has been prepared as described in example 5 of WO 03/051934 whilst using an asymmetric metallocene dimethylsilyl [(2- methyl-(4'-tert.butyl)-4-phenyl-indenyl)(2-isopropyl-(4'-tert.butyl)-4-phenyl- indenyl)]zirkonium dichloride.
  • Such catalyst has been used to polymerise a polypropylene copolymer with 4 mol % ethylene in the Borstar process, known in the art.
  • the materials have been pelletized together with additives, i.e. 1000 ppm of a commercial stabilizer Irganox B215 (supplied by Ciba), using an extruder at melt temperature of 240 °C.
  • the pelletized materials have been used for film blowing at a commercial blown-film line Alpine 35, using a barrier screw with temperature settings 180/200/220/220/220 °C and a initial screw speed of 60 rpm and 80 rpm, respectively.
  • the bubble has been stretched with a blow up ratio of 2 and winded up with 10.4 m/min. Please confer to Table 4 for the settings for film blowing.
  • Table 4 for the settings for film blowing.
  • the film from El behaves significantly different to the known polymers.
  • the film is much more transparent and easier to process.
  • frost-line i.e. the transition from transparent melted material to (partly) crystallized film (slightly opaque) is moved to much higher values.
  • the frost line of Cl is observed at 180 mm whereas the frost line of El is at 300 mm. Also the bubble was much more stable. This indicates improved processibility already (as proven further below, see Table 8).
  • E2, E3 and E4 are polymerised using the metallocene catalyst as described in example El but with varying ethylene concentrations to obtain homopolymers (E2, E3) and a copolymer (E4). Please confer to the table 7 for the polymers' properties.
  • C2, C3 and C4 have been prepared with the same process as for Cl and using the same catalyst as described in Cl but with varying ethylene concentrations to obtain a homopolymer (C2) and two copolymers (C3, C4). Please confer to the table 7 for the polymers' properties.
  • C6 has a MFR230/2.16 of 3.3 g/10min, a tensile modulus of 1950 MPa and a branching index g' of 0.7 ("C6").
  • C7 has a MFR230/2.16 of 4.0 g/10min, a tensile modulus of 1950 MPa and a branching index g' of 0.7 ("C7"), respectively.
  • HMS-PPs of different melt flow rates have been used to make blown films.
  • the inventive material shows much higher stable output at same MFR compared to known systems (see Figure 6). It showed that the inventive material El is superior in its processing properties with several respect: First, the bubble stability (a critical parameter for blown film making with linear polypropylenes) is significantly enhanced with the multibranched polypropylenes.
  • the maximum output which can be achieved is higher by 50 % compared to Z/N systems (Cl ) and higher by 20 % compared with HMS-PP (C5 to C7).
  • this is an important finding since it allows utilizing the assets of blown-film makers much more efficient and hence reduces total production costs.

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Abstract

La présente invention porte sur un film soufflé comprenant un polypropylène à ramifications multiples présentant un indice de ramification g' inférieur à 1,00.
PCT/EP2007/007468 2006-08-25 2007-08-24 Film soufflé de polypropylène WO2008022802A1 (fr)

Priority Applications (7)

Application Number Priority Date Filing Date Title
DE602007004630T DE602007004630D1 (de) 2006-08-25 2007-08-24 Blasfolie aus polypropylen
EA200970221A EA200970221A1 (ru) 2006-08-25 2007-08-24 Полипропиленовая плёнка, полученная экструдированием с раздувом
BRPI0717001-7A BRPI0717001A2 (pt) 2006-08-25 2007-08-24 Filme soprado de polipropileno
AT07801893T ATE456608T1 (de) 2006-08-25 2007-08-24 Blasfolie aus polypropylen
CN2007800290360A CN101501110B (zh) 2006-08-25 2007-08-24 聚丙烯的吹塑薄膜
EP07801893A EP2054464B1 (fr) 2006-08-25 2007-08-24 Film soufflé de polypropylène
US12/367,799 US20090182105A1 (en) 2006-08-25 2009-02-09 Blown film of polypropylene

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EP06017789.6 2006-08-25
EP06017789A EP1903070B9 (fr) 2006-08-25 2006-08-25 Film soufflé de polypropylene

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EP (2) EP1903070B9 (fr)
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CN (1) CN101501110B (fr)
AT (2) ATE439393T1 (fr)
BR (1) BRPI0717001A2 (fr)
DE (2) DE602006008470D1 (fr)
EA (1) EA200970221A1 (fr)
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EP2679630A1 (fr) 2012-06-28 2014-01-01 Borealis AG Polypropylène à résistance élevée à la fusion de qualité améliorée
WO2014016206A1 (fr) 2012-07-25 2014-01-30 Borealis Ag Film d'indice de gel ocs faible
EP3018155A1 (fr) 2014-11-05 2016-05-11 Borealis AG Polypropylène ramifié pour des applications de films

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US9938400B2 (en) * 2008-04-23 2018-04-10 Exxonmobil Chemical Patents Inc. Propylene copolymers in soft thermoplastic blends
EP2133389A1 (fr) 2008-06-12 2009-12-16 Borealis AG Composition de polypropylène
EP2147939A1 (fr) 2008-07-22 2010-01-27 Borealis AG Composition de polypropylène avec optiques améliorées pour films et applications de moulage
EP2319885B1 (fr) 2009-10-29 2011-12-21 Borealis AG Résine de polypropylène hétérophase ayant des ramifications à chaînes longues
EP2386584A1 (fr) 2010-05-11 2011-11-16 Borealis AG Composition de polypropylène adaptée au revêtement par extrusion
EP2603548A1 (fr) 2010-08-12 2013-06-19 Borealis AG Film de polypropylène facile à déchirer sans entaille
EP2418237A1 (fr) 2010-08-12 2012-02-15 Borealis AG Film de polypropylène facile à déchirer sans entaille
EP2492293B1 (fr) 2011-02-28 2017-09-20 Borealis AG Composition de polypropylène adaptée au revêtement par extrusion
EP2586824B1 (fr) * 2011-10-31 2016-09-14 Borealis AG Mélange de polypropylène doté d'un équilibre amélioré entre la température d'auto-inflammation et le point de fusion
WO2014088856A1 (fr) * 2012-12-03 2014-06-12 Exxonmobil Chemical Patents Inc. Polymères de propylène
EP2829397A1 (fr) * 2013-07-22 2015-01-28 Basell Poliolefine Italia S.r.l. Films de polyoléfine thermosoudable et feuilles
EP3140329B1 (fr) * 2014-05-06 2019-07-24 Basell Poliolefine Italia S.r.l. Copolymères de propylène-éthylène aléatoire et leur procédé de préparation
CN106255720B (zh) * 2014-05-06 2020-04-07 巴塞尔聚烯烃意大利有限公司 多层膜无规丙烯-乙烯共聚物
KR101764561B1 (ko) * 2014-05-06 2017-08-02 바셀 폴리올레핀 이탈리아 에스.알.엘 랜덤 프로필렌-에틸렌 공중합체 및 이의 제조 방법
EP3334602A4 (fr) 2015-08-13 2019-01-09 ExxonMobil Chemical Patents Inc. Feuilles multicouche comprenant un polypropylène à résistance à l'état fondu élevée

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EP2679630A1 (fr) 2012-06-28 2014-01-01 Borealis AG Polypropylène à résistance élevée à la fusion de qualité améliorée
WO2014001394A1 (fr) 2012-06-28 2014-01-03 Borealis Ag Polypropylène à haute résistance à l'état fondu de qualité améliorée
US9410034B2 (en) 2012-06-28 2016-08-09 Borealis Ag High melt strength polypropylene of improved quality
WO2014016206A1 (fr) 2012-07-25 2014-01-30 Borealis Ag Film d'indice de gel ocs faible
US9376549B2 (en) 2012-07-25 2016-06-28 Borealis Ag Film with low OCS gel index
EP3018155A1 (fr) 2014-11-05 2016-05-11 Borealis AG Polypropylène ramifié pour des applications de films
WO2016071400A1 (fr) 2014-11-05 2016-05-12 Borealis Ag Polypropylène ramifié destiné à des applications de films

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DE602007004630D1 (de) 2010-03-18
DE602006008470D1 (de) 2009-09-24
CN101501110A (zh) 2009-08-05
EA200970221A1 (ru) 2009-08-28
EP2054464B1 (fr) 2010-01-27
US20090182105A1 (en) 2009-07-16
CN101501110B (zh) 2013-02-20
KR20090016609A (ko) 2009-02-16
ATE439393T1 (de) 2009-08-15
ES2340436T3 (es) 2010-06-02
ATE456608T1 (de) 2010-02-15
ES2331091T3 (es) 2009-12-21
EP2054464A1 (fr) 2009-05-06
EP1903070B9 (fr) 2009-12-23
KR101032013B1 (ko) 2011-05-02
EP1903070A1 (fr) 2008-03-26
EP1903070B1 (fr) 2009-08-12
BRPI0717001A2 (pt) 2013-10-08

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